Method for purifying nitric oxide
A nitric oxide and refining method technology, applied in nitric oxide, chemical instruments and methods, separation methods, etc., can solve the problems of liquid nitric oxide explosion, expensive equipment, complex cooling operation, etc.
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Embodiment 1
[0047] In embodiment 1, omit above-mentioned implementation mode ( figure 1 ) in the absorbing liquid contact device 1 performs an adsorption process on the crude NO gas supplied from the NO cartridge Y1 with the adsorption tube 2 . Activated alumina (trade name: KHD-12, manufactured by Sumitomo Chemical Co., Ltd.) was used as the inorganic adsorbent filled in the adsorption tube 2 . As pretreatment of the adsorbent, 18.6 g of activated alumina and 0.3 N of nitric acid aqueous solution were mixed and stirred at 40° C. for 2 hours, and then vacuum-dried at 60° C. for 6 hours. The pretreated adsorbent obtained in this way is filled in the adsorption tube 2 (a stainless steel cylindrical adsorption tube with an inner diameter of 7.5 mm and a length of 500 mm. After that, the temperature of the adsorption tube 2 is raised to 150° C. and the on-off valves 4A to 4D are closed. state and the on-off valve 4E is in the open state, the vacuum pump 8 is operated, and the vacuum is carri...
Embodiment 2
[0049] In Example 2, molecular sieve 4A (trade name: Zeolum A-4, manufactured by Tosoh Corporation) was used instead of the activated alumina of Example 1 as the inorganic adsorbent. NO purification (pretreatment and adsorption steps) was carried out in the same manner as in Example 1 except that the inorganic adsorbent was changed. When 1 hour has elapsed after the flow of the raw material gas to the adsorption tube 2 has passed, the result of analyzing the non-adsorbed gas derived from the adsorption tube 2 is, H 2 O content = 1ppm, NO 2 Content=25ppm, N 2 O content = 60ppm, N before and after circulation 2 O content increment is 10ppm.
Embodiment 3
[0051] In Example 3, as pretreatment of the adsorbent, 150 ml of activated alumina (trade name: KHD-12, manufactured by Sumitomo Chemical Co., Ltd.) was placed in a stainless steel autoclave with an inner capacity of 300 ml and a pressure resistance of 3 MPa, and added NO / NO 2 =1 / 1 mixed gas up to 1.5MPaG. After 4 hours at 40°C, purge gas was introduced and NO / NO was added again 2 =1 / 1 mixed gas up to 1.5MPaG, keep at 30°C for 5 hours. The adsorbent thus pretreated was filled in the same adsorption tube 2 as in Example 1, and purified in the same manner as in Example 1 for supplying the raw material gas. When 1 hour has elapsed after the start of circulation, the result of analyzing the non-adsorbed gas derived from the adsorption tube 2 is, H 2 O content = 1ppm, NO 2 Content=30ppm, N 2 O content = 63ppm, N before and after circulation 2The O content increment was 13 ppm.
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